JP3770036B2 - Toner for electrophotography and method for producing the same - Google Patents
Toner for electrophotography and method for producing the same Download PDFInfo
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- JP3770036B2 JP3770036B2 JP2000062146A JP2000062146A JP3770036B2 JP 3770036 B2 JP3770036 B2 JP 3770036B2 JP 2000062146 A JP2000062146 A JP 2000062146A JP 2000062146 A JP2000062146 A JP 2000062146A JP 3770036 B2 JP3770036 B2 JP 3770036B2
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- toner
- release agent
- temperature
- organic solvent
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Description
【0001】
【発明の属する技術分野】
本発明は電子写真用トナーに関する。
【0002】
【従来の技術】
電子写真式複写機やプリンター等の画像形成装置においてトナー像を記録紙上に定着する方法としては一般に、ヒートローラやベルト部材による加熱圧着方式が多く採用されている。この方式は比較的コンパクトなシステムでありながら、熱効率がよく、高速定着が可能であるという利点がある。しかし、この方式では、加熱溶融されたトナーは高い圧力でヒートローラに接触するため、記録紙上のトナー像の一部が定着部材に付着してトナー像に欠損が生じ、その定着部材に付着したトナーが次の定着の際、記録紙上に転写されるといういわゆるオフセット現象が問題となっていた。このため、定着部材の表面材料として表面剥離性の優れたフッ素材料やシリコーン材料を用い、更には表面に離型性の良いシリコーンオイルを塗布してオフセットを防止していた。しかし、表面材料の選択だけではオフセットの防止は不十分であり、オイル塗布方式では過剰なオイルが記録紙を汚したり、記録部材に浸透し耐久寿命を低下させる等の問題があった。また、オイル供給・塗布装置を設置するためコストアップになっていた。さらには、オフセットを防止できたとしてもその温度幅(非オフセット温度域)が狭いため、定着温度の変化により再びオフセットが発生するという問題が生じていた。近年複写機やプリンターの高速化、省エネルギー化のため、低温定着化が望まれているが、このオフセットのため十分に成果を上げていないのが実状である。
【0003】
そこで、特開平10-207116号公報では表面に露出するワックスの量とワックスの平均分散粒径を規定したトナーを用い、トナーとしての粉体特性を維持しながらオイルレス定着性能を達成する試みがなされている。特に、ワックスの平均分散粒径は0.1〜2μmである。
【0004】
【発明が解決しようとする課題】
しかしながら、上記のトナーはワックスの平均分散粒径が大きく、特に最大粒径はさらに大きいため、得られた画像をオーバーヘッドプロジェクタ(OHP)に適用すると、画像を光がほとんど透過せず、そのOHP透光性に問題が生じていた。特に、オイルレス定着を達成できる多量のワックスを添加したトナーを用いると、OHP透光性の悪化は顕著であった。また、上記トナーではワックスを積極的に表面に露出させるため、ワックス粒子がトナーから脱落しやすく、連続複写したときの耐久性の低下が顕著であった。すなわち、上記トナーを用いて連続複写すると、トナー流動性が悪化して帯電性が低下したり、画像濃度、粒状性およびカブリ等の画質性能の低下が顕著であった。
【0005】
本発明は上記事情に鑑みなされたものであり、オフセットが発生しない定着温度幅が比較的広く、OHP透光性に優れ、長期にわたって帯電性および画質に優れたトナーおよびその製造方法を提供することを目的とする。
【0006】
【課題を解決するための手段】
本発明は少なくとも結着樹脂、着色剤および離型剤を含み、離型剤が粒子中、平均粒径0.1μm以下かつ最大粒径0.4μm以下で分散していることを特徴とする電子写真用トナーに関する。
【0007】
本発明はまた、少なくとも結着樹脂または重合性モノマー、着色剤および離型剤を有機溶剤に溶解・分散してなる油性相を調製する調液工程、
油性相を水性相中に分散して油性相からなる液滴粒子の造粒を行う造粒工程、および
液滴粒子から有機溶剤を除去する脱溶工程または液滴粒子中の重合性モノマーを重合しながら液滴粒子から有機溶剤を除去する重合−脱溶工程を含み、
調液工程、造粒工程、および脱溶工程または重合−脱溶工程を離型剤が溶媒に溶解する温度以上で行うことを特徴とする電子写真用トナーの製造方法に関する。
【0008】
【発明の実施の態様】
本発明のトナーは少なくとも結着樹脂、着色剤および離型剤を含有し、かつ離型剤が粒子中において平均粒径0.1μm以下、好ましくは0.01〜0.085μm、最大粒径0.4μm以下、好ましくは0.05〜0.4μmで分散している。本発明のトナーにおいてはこのように離型剤が微分散しているため、オイルレス定着方式を採用した場合であっても、低温オフセットが改善し、低温定着性が向上するだけでなく、オフセットが発生しない定着温度幅が比較的広くなる。また、一般に不透明な離型剤を用いた場合であっても可視光(波長約0.4μm以上)が透過する割合が増加するため、OHP透光性が向上し、カラー複写機、カラープリンター用トナーとしての使用に適している。さらに離型剤はトナー粒子中に微分散され、離型剤のトナーからの脱落が回避されるため、長期にわたって良好な帯電性および画質性を維持できる。
【0009】
離型剤の平均分散粒径が0.1μmを越えたり、最大粒径が0.4μmを越えると、オフセットが発生し易くなり、非オフセット温度域が狭まる。また、当該トナーを用いて得られた画像をオーバーヘッドプロジェクタ(OHP)に適用すると、画像を可視光がほとんど透過せず、そのOHP透光性が問題となる。さらには、離型剤のトナーからの脱離が顕著になるため、耐久性に問題が生じ、すなわち長期の使用によって帯電性が低下したり、画像濃度、粒状性およびカブリ等の画質性能が低下する。
【0010】
トナー中における離型剤の平均分散粒径および最大粒径は以下のようにして測定することができる。トナーをエポキシ等の樹脂で固化し、ミクロトームにて1000オングストローム程度の厚さにスライスし、透過型電子顕微鏡で観察することにより相分離した離型剤の粒の分散粒径を測定することができる。本発明において平均分散粒径は任意の50個の離型剤粒子の分散粒径から求め、最大粒径は任意の100個の離型剤粒子から求める。
【0011】
本発明のトナーは上記のようなトナーが得られれば、いかなる方法によって製造されてよいが、公知の湿式法において一連の工程を離型剤が溶媒に溶解する温度以上で行うことによって本発明のトナーを有効に得ることができる。すなわち、本発明のトナーは、
(I)少なくとも結着樹脂または重合性モノマー、着色剤および離型剤を有機溶剤に溶解・分散してなる油性相を調製する調液工程、
(II)油性相を水性相中に分散して油性相からなる液滴粒子の造粒を行う造粒工程、および
(III)液滴粒子から有機溶剤を除去する脱溶工程または(IV)液滴粒子中の重合性モノマーを重合しながら液滴粒子から有機溶剤を除去する重合−脱溶工程を含み、
調液工程(I)、造粒工程(II)、および脱溶工程(III)または重合−脱溶工程(IV)を離型剤が溶媒に溶解する温度以上で行うことを特徴とする電子写真用トナーの製造方法によって有効に得ることができる。このように、湿式法において上記工程を離型剤が溶媒に溶解する温度以上で行うことにより、すなわち上記工程を離型剤が溶解された状態で行うことにより、最終の脱溶工程または重合−脱溶工程において離型剤が析出し、このとき同時に、溶解している結着樹脂または生成した結着樹脂の存在により液滴中の粘度が上がるため、離型剤は粗大粒子まで成長したり、凝集することなく、微分散したトナーを得ることができると考えられる。調液工程(I)のみで溶媒中、離型剤が溶解あるいは微分散されていても、造粒工程(II)ならびに脱溶工程(III)または重合−脱溶工程(IV)で、系中の温度が、離型剤が溶媒に溶解する温度より低いと、溶媒に対する離型剤溶解度が低下するため、微分散されていた離型剤は成長して凝集し、また溶解されていた離型剤は析出、成長して凝集し、本発明のトナーを得ることができない。特に、脱溶工程の温度が低いと、溶媒の蒸発に伴い、樹脂はまだ溶解し粘度が低い状態で離型剤は急激に再結晶するため凝集する。
以下、湿式法を採用して本発明のトナーを得る場合について詳しく説明する。
【0012】
本発明のトナーは重合過程を含まない湿式法、または重合過程を含む湿式法、いずれの湿式法においても得ることができる。
【0013】
重合過程を含まない湿式法、例えば、乳化分散造粒法を用いて本発明のトナーを製造する場合、本発明のトナーは、
(I)少なくとも結着樹脂、着色剤および離型剤を有機溶剤に溶解・分散してなる油性相を調製する調液工程、
(II)油性相を水性相中に分散して油性相からなる液滴粒子の造粒を行う造粒工程、および
(III)液滴粒子から有機溶剤を除去する脱溶工程を行うに際して、
調液工程(I)、造粒工程(II)、および脱溶工程(III)を、離型剤が溶媒に溶解する温度以上で行うことにより得ることができる。
【0014】
具体的にはまず、少なくとも結着樹脂、着色剤および離型剤を有機溶剤に溶解・分散してなる油性相を調製する(調液工程(I))。本発明において油性相は離型剤が溶媒(有機溶剤)に溶解する温度以上で調製され、当該油性相中、離型剤は溶解されている。油性相の調製に際しては、結果的に離型剤が溶解された油性相が調製されればよく、例えば、所定の温度を有する有機溶剤に上記トナー成分を添加し、混合・撹拌してもよいし、または常温の有機溶剤に上記トナー成分を添加し、所定温度に加熱しながら混合・撹拌してもよい。
【0015】
本発明において使用可能な離型剤としては、加温によって有機溶剤に溶解できるものであれば特に制限されず、トナーの分野で公知の離型剤、例えば、合成ワックス、天然ワックスおよびロウ類等が使用可能である。これらの離型剤の中でも、耐オフセット性改良の観点から、有機溶剤に常温以上90℃以下の温度で溶解する離型剤を使用することが好ましい。具体的には使用される溶媒に対して常温以上90℃以下、好ましくは25〜60℃のいずれかの温度で3.5重量%以上、好ましくは10重量%以上、より好ましくは15重量%以上の濃度(離型剤/(離型剤+溶媒))で溶解するような離型剤を用いることが好ましい。また、トナー耐熱性および低温定着性の観点からは、融点が60〜120℃であることが好ましい。
【0016】
具体的には合成ワックスとして、例えば、合成炭化水素のフィッシャートロプシュ、ポリエチレン、ポリプロピレン等のワックス、その変性ワックスとしてモンタン、パラフィン、マイクロクリスタリン等のワックス、エステル、脂肪酸、酸アミド、ケトン等のワックス等が挙げられる。また、天然ワックスとして、例えば、植物系のカルナウバ、キャンデリラ、ライス等のワックス、ホホバ油等が挙げられる。その他動物系および鉱物系のワックスも使用可能である。特に融点および有機溶剤に対する溶解度の点でエステル、モンタン、ケトン等の合成ワックス、カルナウバ等の天然ワックスが本発明に適している。
【0017】
離型剤の添加量は、トナーの耐熱性および耐ストレス性ならびに帯電性能の観点から、結着樹脂100重量部に対し3〜30重量部、好ましくは10〜25重量部が好適である。従来ではオイルレス定着を達成できる程度の量のワックスを添加すると、OHP透光性が悪化していたが、本発明においては上記のようにワックスを比較的多く添加してもそのような問題は生じない。
【0018】
本発明において使用可能な有機溶剤としては、離型剤を溶解できる公知の有機溶剤であれば特に制限されず、例えば、トルエン、キシレン等の芳香族溶媒、酢酸エチル、酢酸ブチル等のエステル系溶媒、アセトン、メチルエチルケトン等のケトン系溶媒、イソプロピルアルコール、n−ブタノール、エタノール等のアルコール系溶媒、クロロホルム、四塩化炭素等のハロゲン系溶媒が挙げられる。これらの有機溶剤は単独でまたは2種以上混合して用いてよい。これらの溶剤は後述の造粒工程での造粒に悪影響を及ぼさない範囲で油性相中50〜95重量%の割合で使用される。
【0019】
離型剤としてエステルワックスまたはカルナバワックスを用いる場合、有機溶剤としてトルエンを用いることが好ましい。
【0020】
油性相が調製される温度は離型剤が有機溶剤に溶解できれば特に制限されず、使用される離型剤と有機溶剤の種類に依存して適宜選択される。当該温度をあまり高く設定しても製造効率の観点から好ましくないため、通常、常温以上90℃以下、好ましくは25〜80℃の範囲内で設定される。例えば、離型剤としてエステルワックスまたはカルナバワックスを用い、有機溶剤としてトルエンを用いる場合、35〜70℃、好ましくは40〜60℃が望ましい。
【0021】
結着樹脂としては、上記有機溶剤に溶解可能な樹脂が使用可能であり、例えば、ポリエステル系樹脂、スチレン系樹脂、(メタ)アクリル系樹脂、スチレン−(メタ)アクリル系共重合体樹脂、オレフィン系樹脂、ポリアミド系樹脂、ポリカーボネート樹脂、ポリエーテル樹脂、ポリ酢酸ビニル系樹脂、ポリスルフォン樹脂、エポキシ樹脂、ポリウレタン樹脂などの、公知の各種の樹脂を1種または2種以上使用することが可能である。本発明においては、離型剤のさらなる微分散、溶媒に対する溶解性、トナー定着性能、透光性、耐熱性の観点から、ポリエステル系樹脂を用いることが好ましく、ポリエステル系樹脂を用いる場合、数平均分子量(Mn)が2000〜8000、重量平均分子量/数平均分子量(Mw/Mn)が5〜20、およびガラス転移点が55〜70℃のポリエステル樹脂を用いることがより好ましい。このようなポリエステル樹脂は上記有機溶剤により溶解しやすく、また、離型剤を添加しても、OHP透光性がより有効に維持されながら、耐低・高温オフセット性および定着性能が有効に向上するためである。また、トナーとして必要な耐熱性および耐ストレス性も有効に維持される。
【0022】
本発明においては離型剤としてエステルワックスまたはカルナバワックスを用いる場合、結着樹脂としてポリエステル樹脂を用いることが好ましい。離型剤と結着樹脂との相溶性が良好なため、離型剤の微分散がより有効に達成され、また樹脂とワックスの屈折率が近いため透光性がより向上するからである。
【0023】
着色剤としては特に制限されず、従来からトナーの着色剤として使用されている公知の顔料・染料が使用可能である。
黒色顔料としては、例えば、カーボンブラック、酸化銅、二酸化マンガン、アニリンブラック、活性炭、非磁性フェライト、磁性フェライト、マグネタイトなどがある。
黄色顔料としては、例えば、黄鉛、亜鉛黄、カドミウムイエロー、黄色酸化鉄、ミネラルファストイエロー、ニッケルチタンイエロー、ベンジジンイエローG、などがある。
橙色顔料としては、例えば、赤色黄鉛、モリブデンオレンジ、パーマネントオレンジGTR、パラゾロンオレンジ、バルカンオレンジなどがある。
赤色顔料としては、例えば、ベンガラ、カドミウムレッド、鉛丹、硫化水銀、カドミウム、パーマネントレッド4R、リソールレッド、ピラゾロンレッド、ウオッチングレッド、カルシウム塩、レーキレッドC、レーキレッドD、ブリリアントカーミン6Bなどがある。
【0024】
青色顔料としては、例えば、紺青、コバルトブルー、アルカリブルーレーキ、ビクトリアルブルーレーキ、フタロシアニンブルー、無金属フタロシアニンブルー、フタロシアニンブルーなどがある。
体質顔料としては、例えば、バライト粉、炭酸バリウム、クレー、シリカ、ホワイトカーボン、タルク、アルミナホワイトなどがある。
これらの着色剤は、単独あるいは複数組み合せて用いることができるが、通常、上記結着樹脂100重量部に対して、1〜20重量部、好ましくは2〜15重量部使用することが望ましい。
【0025】
油性相には荷電制御剤が溶解または微分散されていてもよい。荷電制御剤(CCA)としては、上記の有機溶剤に溶解あるいは微分散できるものであれば全て適用できる。負荷電制御剤としては、例えば、含金属錯塩ボントロンE81、E84(オリエント化学社製)、LR147(日本カーリット社製)、チオインジゴ系顔料、カリックスアレーン系化合物ボントロンE89(オリエント化学社製)、含フッ素化合物コピーチャージNX VP434(ヘキスト社製)、FT-310(ネオス社製)等が挙げられる。正荷電制御剤としては、例えば、第4級アンモニウム塩P-51(オリエント化学社製)、コピーチャージPX VP435(ヘキスト社製)などが挙げられる。カラートナー用としては色調を損なうことのない透明色から白色の摩擦帯電により正または負の荷電を与え得る物質がよい。これらを1種あるいは2種以上用いてもよい。荷電制御剤の添加量は特に制限されないが、結着樹脂100重量部に対して0.1〜4重量部、好ましくは0.5〜2重量部が好適である。
【0026】
次いで、得られた油性相を水性相中に分散して油性相からなる液滴粒子の造粒を行う(造粒工程(II))。すなわち、水性相中に油性相からなる液状粒子が分散された分散系(O/Wエマルジョン)を調製する。本発明において造粒は、液滴中に溶解されている離型剤が析出しない程度の温度で行われ、すなわち離型剤が溶媒(有機溶剤)に溶解する温度以上で行われる。通常、造粒は調液工程の温度を維持しながら行われる。そのため、分散時においては油性相および水性相をそれぞれ所定温度に制御した後で、これらを混合し、分散・造粒することが好ましい。
【0027】
造粒に際しては、油性相を水性相に添加し、乳化させ、油性相を水性相中に分散してもよいし、または水性相を油性相に添加し、転相乳化させ、油性相を水性相中に分散してもよい。
【0028】
水性相は水に、所望により分散剤および/または分散助剤等の添加剤を添加してなる。分散剤としては水性相中で親水性コロイドとなるものが好ましく、特にゼラチン、アラビアゴム、寒天、セルローズ誘導体、合成高分子(例えばポリビニルアルコール、ポリビニルピロリドン、ポリアクリル酸塩、ポリメタクリル酸塩等)、難溶性無機塩(例えばリン酸カルシウム)、親水性シリカ等が挙げられる。分散助剤として通常界面活性剤が用いられ、アポニン等の天然界面活性剤、アルキレンオキサイド系、グリセリン系あるいはグリシドール系等のノニオン系界面活性剤、カルボン酸、スルホン酸、リン酸、硫酸エステル基、リン酸エステル基等の酸性基含有のアニオン系界面活性剤等が挙げられる。
【0029】
水性相中における分散剤および分散助剤の濃度は特に制限されず、一般に、それぞれ1〜10重量%、0.001〜1重量%が好適である。
【0030】
油性相の水性相への分散に際しては、得られるトナー粒子が所望粒径になるよう、油性相の液状粒子の径を撹拌によって制御することが好ましい。油性相と水性相との混合体積比(油性相/水性相)は、乳化安定性を考慮して1/1〜1/4の間で選択できる。
【0031】
油性相からなる液滴粒子を造粒した後は、当該液滴粒子から有機溶剤を除去する(脱溶工程(III))。脱溶は、系中温度の低下に伴う有機溶剤の離型剤溶解度の低下によって離型剤が析出することがない程度の温度で行われればよく、通常、離型剤が溶媒(有機溶剤)に溶解する温度以上で行われ、好ましくは調液工程の温度を維持しながら長時間かけて行われる。このように系中温度の低下(溶解度の低下)による離型剤の析出を回避しながら脱溶を行うことにより、溶剤除去による離型剤の析出のみが起こり、同時に液滴粒子中において脱溶による粘度上昇が起こるため、トナー中において析出された離型剤微粒子は成長または凝集することなく微分散できると考えられる。
【0032】
本発明においては脱溶工程を長時間かけて行うことが好ましい。離型剤がより有効に微分散できるためである。有機溶剤、離型剤、樹脂の各種類で異なるため限定できない。
【0033】
有機溶剤の除去が完了した後は、冷却後、ろ過/水洗を数回繰り返し行い、乾燥・解砕を行い、本発明のトナーを得ることができる。
【0034】
また、本発明のトナーは、重合過程を含む湿式法、例えば、懸濁重合法、乳化重合法、乳化重合凝集法、シード重合法、界面重合法等を採用して得ることもできる。以下、重合過程を含む湿式法を採用して本発明のトナーを得る場合について説明するが、特記しない限り、上記の重合過程を含まない湿式法を採用する場合と同様とする。なお、重合過程を含む湿式法においては重合性モノマーも「溶媒」として作用するため、「溶媒」は「有機溶剤と重合性モノマーとの混合溶媒」を意味するものとする。また、添加量については「結着樹脂100重量部」を「重合性モノマー100重量部」に読み替えて適用するものとする。
【0035】
重合過程を含む湿式法、特に懸濁重合法を用いて本発明のトナーを製造する場合、本発明のトナーは、
(I)少なくとも重合性モノマー、着色剤および離型剤を有機溶剤に溶解・分散してなる油性相を調製する調液工程、
(II)油性相を水性相中に分散して油性相からなる液滴粒子の造粒を行う造粒工程、および
(IV)液滴粒子中の重合性モノマーを重合しながら液滴粒子から有機溶剤を除去する重合−脱溶工程を行うに際して、
調液工程(I)、造粒工程(II)、および重合−脱溶工程(IV)を、離型剤が溶媒に溶解する温度以上で行うことにより得ることができる。
【0036】
具体的にはまず、少なくとも重合性モノマー、着色剤および離型剤を有機溶剤に溶解・分散してなる油性相を調製する(調液工程(I))。重合過程を含む湿式法においては、油性相は離型剤が溶媒、すなわち有機溶剤と重合性モノマーとの混合溶媒に溶解する温度以上で調製され、当該油性相中、離型剤は溶解されている。
【0037】
有機溶剤は、通常、油性相中5重量%以上の割合で使用されるが、使用されなくてもよい。有機溶剤が使用されない場合において、油性相は離型剤が重合性モノマーに溶解する温度以上で調製される。
【0038】
重合性モノマーとしては、前記の結着樹脂を構成でき、かつ疎水性を有すれば特に制限されず、例えば、スチレン系樹脂、(メタ)アクリル系樹脂、スチレン−(メタ)アクリル系共重合体樹脂等の原料となるビニル系モノマー等が挙げられる。
【0039】
油性相には重合開始剤が添加されていることが好ましい。重合開始剤としては、例えば、アゾ化合物系、ハイドロパーオキサイド系、レドックス系等のラジカル重合開始剤が挙げられる。
【0040】
次いで、得られた油性相を水性相中に分散して油性相からなる液滴粒子の造粒を行う(造粒工程(II))。本発明において造粒は、液滴中に溶解されている離型剤が析出しない程度の温度で行われ、すなわち離型剤が溶媒(有機溶剤と重合性モノマーとの混合溶媒)に溶解する温度以上で行われる。通常、造粒は調液工程の温度を維持しながら行われる。有機溶剤が使用されない場合において、造粒は離型剤が重合性モノマーに溶解する温度以上で行われる。
【0041】
次いで、液滴粒子中の重合性モノマーを重合しながら液滴粒子から有機溶剤を除去する(重合−脱溶工程(IV))。すなわち、当該工程においては、重合を行いながら脱溶を行い、結果として重合終了時において脱溶が完了している。
【0042】
重合−脱溶は、系中温度の低下に伴う離型剤溶解度の低下によって離型剤が析出することがない程度の温度で行われ、すなわち離型剤が溶媒(有機溶剤と重合性モノマーとの混合溶媒)に溶解する温度以上で行われる。有機溶剤が使用されない場合において、重合−脱溶は離型剤が重合性モノマーに溶解する温度以上で行われる。このように系中温度の低下(溶解度の低下)による離型剤の析出を回避しながら重合−脱溶を行うことにより、溶剤の除去と樹脂の生成による離型剤の析出のみが起こり、同時に液滴粒子中において溶剤の除去と樹脂の生成による粘度上昇が起こるため、トナー中において析出された離型剤微粒子は成長または凝集することなく微分散できると考えられる。
【0043】
詳しくは、重合−脱溶工程の温度および時間等の条件は、温度について上記要件を満たす限り、特に制限されないが、前記結着樹脂の説明で記載したMn、Mw/Mnおよびガラス転移点を有する樹脂が得られるような条件とすることが好ましい。
【0044】
本発明においては重合−脱溶工程を長時間かけて行うことが好ましい。離型剤がより有効に微分散できるためである。
【0045】
有機溶剤の除去が完了した後は、冷却後、ろ過/水洗を数回繰り返し行い、乾燥・解砕を行い、本発明のトナーを得ることができる。
【0046】
以上のような製造方法によって製造され得る本発明のトナーは体積平均粒径3〜10μm、好ましくは4〜8μmに制御されていることが望ましい。
【0047】
本発明のトナーは、流動性、帯電性、耐熱性等の向上の観点から、微粒子によって表面処理されることが好ましい。微粒子の材料としては、従来から電子写真の分野でトナーに外添される公知の微粒子材料が使用可能であり、例えば、金属酸化物、金属間化合物、樹脂等が挙げられる。具体例として、金属酸化物としては、例えば、シリカ、酸化チタン、アルミナ、ジルコニア等が挙げられる。金属間化合物としては、例えば、チタン酸ストロンチウム、炭化ケイ素、窒化ケイ素等が挙げられる。樹脂としては、例えば、高分子フッ化物、シリコーン化合物、アクリル系樹脂等が挙げられる。上記微粒子の添加量はトナー100重量部に対して0.2〜3重量部が適当である。
【0048】
本発明のトナーは比較的多量の離型剤を微分散状態で含有できるため、オイルレス定着方式を採用した複写機において使用しても、本発明の目的を有効に達成できる。
【0049】
また、本発明のトナーは、キャリアと共に使用する二成分現像用トナーとしても、キャリアを使用しない一成分現像用トナーとしても使用することができる。
【0050】
本発明のトナーとともに使用するキャリアとしては、公知のキャリアを使用することができ、例えば、鉄粉、フェライト等の磁性粒子よりなるキャリア、磁性粒子表面を樹脂等の被覆剤で被覆したコート型キャリア、あるいは結着樹脂中に磁性体微粉末を分散してなる分散型キャリア等いずれも使用可能である。
以下、実施例により本発明をさらに詳しく説明する。
【0051】
【実施例】
(実施例1)
数平均分子量Mnが2800、重量平均分子量/数平均分子量(Mw/Mn)が7、Tgが68℃のポリエステル樹脂100gをトルエン360gに溶解後、フタロシアニン顔料5g、荷電制御剤LR147(日本カーリット社製)0.5gとともに2リットルのポリビンにいれ、ウルトラターラックス(IKA社製)で30分混合、分散させた後、融点80℃のエステルワックスHOE-WAX F(クラリアント社製)20gを入れ、50℃に加温・攪拌し、熱によりワックスがトルエン中に溶解された油性相を調製した。次に、ポリアクリル酸ナトリウム3.5重量%水溶液1100g中にアルキルジフェニルエーテルジスルフォン酸ナトリウム11gを添加して50℃の水性相を調製し、これを50℃に保った油性相中に混合し、混合液を50℃に保持しながらT.Kオートホモミクサー(特殊機化工業社製)で3500rpm、10分攪拌を行い乳化させた。直ちに、50〜55℃の恒温槽中スリーワンモーターで20時間攪拌しトルエンを除去し、冷却後、ろ過/水洗を数回繰り返し行った。洗浄後のトナーケーキをステンレスバットに移し替え、恒温乾燥機にて35℃、48時間、乾燥を行い、ボールミルを用い解砕し、90μmのメッシュでフルイにかけ、平均粒径6.2μmのトナーを得た。透過型電子顕微鏡観察(5万倍)の結果(以下、同様とする)、トナーの粒子内部に平均粒径0.05μm、最大粒径0.23μmのワックス粒子が分散していた。
【0052】
(実施例2)
ワックスとして融点93℃のカルナバ45T-1(日本セイロウ社製)10gを用いたこと以外、実施例1と同様にして、平均粒径が7.5μmのトナーを得た。トナーの粒子内部には平均粒径0.08μm、最大粒径0.37μmのワックス粒子が分散していた。
【0053】
(実施例3)
結着樹脂としてMnが3000、Mw/Mnが9でガラス転移点が60℃のポリエステルを用いたこと以外、実施例1と同様にして平均粒径5.4μmのトナーを得た。トナーの粒子内部には平均粒径0.04μm、最大粒径0.18μmのワックス粒子が分散していた。
【0054】
(比較例1)
ワックスとして融点55℃のn−ヘキサデシルエーテル20gを用いたこと以外、実施例1と同様にして平均粒径が7.0μmのトナーを得た。トナーの粒子内部には平均粒径1.5μm、最大粒径4.8μmのワックス粒子が分散していた。
【0055】
(比較例2)
ワックスとして融点126℃のポリエチレンワックス400P(三井化学社製)2gを用いたこと以外、実施例1と同様にして平均粒径8.6μmのトナーを得た。トナーの粒子内部には平均粒径3.5μm、最大粒径6.2μmのワックス粒子が分散していた。
【0056】
各実施例および比較例で使用したワックスの種類、融点、添加量および濃度と、各温度での各ワックスのトルエンに対する飽和濃度をまとめて表1に示す。
【0057】
【表1】
【0058】
上記の実施例および比較例で得られたトナー100重量部にシリカ微粒子R972(日本アエロジル社製)1.2重量部をヘンシェルミキサ(三井金属鉱山社製)で30m/sの速度で3分間表面処理を行った。後述のキャリアとトナー混合比6重量%で混合して2成分非磁性現像剤を得、各現像剤を以下の評価項目について評価した。
【0059】
(非オフセット温度域)
フルカラー複写機CF900(ミノルタ社製)の定着器を改造し、単独で定着温度を可変制御し通紙、定着できるようにした定着テスターを用いた。定着テスターにより複写した後、様々な定着温度で定着させ、ローラ1周後、オフセットしたトナー像がコピー用紙を汚しているかどうかを目視で評価し、汚染のない上限温度と下限温度を測定した。これらの温度幅が広いほど良好である。
【0060】
(透光性)
上記定着テスターを用いて、非オフセット温度域の中心温度で定着させたOHP用紙上のコピー画像をオーバーヘッドプロジェクターEZ-2(富士写真フィルム社製)で目視評価した。
○:透明で色濁りなく良好であった;
×:不透明で実用上使用不可能であった。
【0061】
結果を以下の表に示す。
【表2】
【0062】
各現像剤を用いてCF900(ミノルタ社製)により1万枚複写し、初期と1万枚複写後の現像剤および複写画像について評価した。
(帯電量)
図1の電界分離方式の帯電量測定装置で、現像剤2gをスリーブ2上にまぶし、-2kvをバイアス電源4でスリーブ2に印加し、スリーブ2を1000rpm、1分間回転し、円筒電極1にトナー7を分離した。分離されたトナー重量(g)、トナー分離時に測定用コンデンサ5に流れ込んだ電荷量(μc)より、帯電量(μc/g)を計算した。
【0063】
(画像濃度)
CF900(ミノルタ社製)による最大濃度のベタ複写画像における任意の10点の濃度をマクベス濃度計(マクベス社製)により測定し、これらの平均値xを求めて以下に従って評価した。
○:1.0<x<1.3
△:0.8<x≦1.0または1.3≦x<1.5
×:x≦0.8または1.5≦x
【0064】
(粒状性)
CF900(ミノルタ社製)による複写画像を目視により観察し、粒状性を以下のランク付けに従って評価した。なお、粒状性とは特に低濃度のベタ画像均一性(キメの良悪)をいう。
○:原稿と遜色なく良好であった;
△:原稿に比べ若干劣るが実用上問題なかった;
×:原稿に比べかなり劣り、実用上使用不可であった。
【0065】
(地肌カブリ)
CF900(ミノルタ社製)による複写画像を目視により観察し、地肌カブリを以下のランク付けに従って評価した。なお、地肌カブリとは複写用紙上、本来の画像部以外に、低帯電・逆帯電のトナーが現像、転写されて発生するトナーによる汚れをいう。
○:カブリが見られず良好;
△:カブリがあるものの実用上問題なかった;
×:実用上使用不可であった。
【0066】
結果を以下に示す。
【表3】
【0067】
キャリア
ポリエステル樹脂バイロン200(東洋紡社製)をトルエン、イソプロパノールの混合溶媒に溶解し、平均径40μmの焼成フェライト粉F300(パウダーテック社製)にスピラコータ(岡田精工社製)で塗布、乾燥した。オーブン中140℃、2時間焼成後、解砕、フルイを行い、平均径42μmのポリエステル樹脂コートのフェライトキャリアを調製した。
【図面の簡単な説明】
【図1】 帯電量の測定に用いた帯電量測定装置の概略構成図を示す。
【符号の説明】
1:円筒電極、2:導電性スリーブ、3:磁性ロール、4:バイアス電極、5:測定用コンデンサ、6:現像剤、7:分離トナー。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an electrophotographic toner.
[0002]
[Prior art]
In general, as a method of fixing a toner image on a recording paper in an image forming apparatus such as an electrophotographic copying machine or a printer, a heat pressing method using a heat roller or a belt member is often employed. Although this method is a relatively compact system, it has the advantages of high thermal efficiency and high-speed fixing. However, in this method, since the heat-melted toner contacts the heat roller at a high pressure, a part of the toner image on the recording paper adheres to the fixing member, and the toner image is defective, and adheres to the fixing member. The so-called offset phenomenon that the toner is transferred onto the recording paper at the time of the next fixing has been a problem. For this reason, a fluorine material or a silicone material having excellent surface releasability is used as the surface material of the fixing member, and further, a silicone oil having a good releasability is applied to the surface to prevent offset. However, the selection of the surface material alone is not sufficient to prevent offset, and the oil application method has problems such as excessive oil staining the recording paper or penetrating into the recording member and reducing the durability life. In addition, the installation of an oil supply / coating device has increased costs. Further, even if the offset can be prevented, the temperature range (non-offset temperature range) is narrow, and thus a problem arises in that the offset occurs again due to a change in the fixing temperature. In recent years, low-temperature fixing has been desired in order to increase the speed and energy saving of copying machines and printers, but the actual situation is that the offset has not produced sufficient results.
[0003]
Therefore, Japanese Patent Application Laid-Open No. 10-207116 has attempted to achieve oil-less fixing performance while maintaining the powder characteristics as a toner, using a toner that defines the amount of wax exposed on the surface and the average dispersed particle size of the wax. Has been made. In particular, the average dispersed particle size of the wax is 0.1 to 2 μm.
[0004]
[Problems to be solved by the invention]
However, since the above toner has a large average dispersed particle size of wax, and especially the maximum particle size is larger, when the obtained image is applied to an overhead projector (OHP), the image hardly transmits light and the OHP transmission There was a problem with light. In particular, when toner containing a large amount of wax capable of achieving oil-less fixing was used, the deterioration of OHP translucency was remarkable. In the toner, since the wax is positively exposed on the surface, the wax particles are easily removed from the toner, and the durability is remarkably lowered when continuously copied. That is, when continuous copying is performed using the above toner, toner fluidity is deteriorated and charging property is lowered, and image quality performance such as image density, graininess, and fog is remarkably lowered.
[0005]
The present invention has been made in view of the above circumstances, and provides a toner having a relatively wide fixing temperature range in which no offset occurs, excellent OHP translucency, excellent chargeability and image quality over a long period of time, and a method for producing the same. With the goal.
[0006]
[Means for Solving the Problems]
The present invention includes at least a binder resin, a colorant, and a release agent, and the release agent is dispersed in the particles with an average particle size of 0.1 μm or less and a maximum particle size of 0.4 μm or less. It relates to toner.
[0007]
The present invention also provides a liquid preparation step for preparing an oily phase obtained by dissolving and dispersing at least a binder resin or a polymerizable monomer, a colorant and a release agent in an organic solvent.
A granulation step of dispersing an oily phase in an aqueous phase to granulate droplet particles comprising the oily phase; and
A desolvation step of removing the organic solvent from the droplet particles or a polymerization-desolubility step of removing the organic solvent from the droplet particles while polymerizing a polymerizable monomer in the droplet particles;
The present invention relates to a method for producing an electrophotographic toner, wherein the liquid preparation step, the granulation step, and the desolubilization step or the polymerization-desolubility step are performed at a temperature equal to or higher than the temperature at which the release agent dissolves in the solvent.
[0008]
BEST MODE FOR CARRYING OUT THE INVENTION
The toner of the present invention contains at least a binder resin, a colorant, and a release agent, and the release agent has an average particle size of 0.1 μm or less, preferably 0.01 to 0.085 μm, and a maximum particle size of 0.4 μm or less, preferably in the particles. Is dispersed at 0.05 to 0.4 μm. In the toner of the present invention, since the release agent is finely dispersed in this way, even when the oilless fixing method is adopted, the low temperature offset is improved and the low temperature fixability is improved. The fixing temperature range in which no occurrence occurs is relatively wide. In addition, even when an opaque release agent is used, the transmission rate of visible light (wavelength of about 0.4 μm or more) increases, so that OHP translucency is improved and toner for color copiers and color printers. Suitable for use as Furthermore, since the release agent is finely dispersed in the toner particles and the release agent is prevented from falling off the toner, good chargeability and image quality can be maintained over a long period of time.
[0009]
When the average dispersed particle size of the release agent exceeds 0.1 μm or the maximum particle size exceeds 0.4 μm, offset is likely to occur, and the non-offset temperature range is narrowed. Further, when an image obtained using the toner is applied to an overhead projector (OHP), visible light hardly transmits through the image, and the OHP translucency becomes a problem. Furthermore, the release of the release agent from the toner becomes prominent, resulting in a problem in durability. That is, the chargeability is lowered by long-term use, and the image quality performance such as image density, graininess and fog is lowered. To do.
[0010]
The average dispersed particle size and maximum particle size of the release agent in the toner can be measured as follows. The dispersed particle size of the phase-separated release agent particles can be measured by solidifying the toner with a resin such as epoxy, slicing it to a thickness of about 1000 angstrom with a microtome, and observing with a transmission electron microscope. . In the present invention, the average dispersed particle size is determined from the dispersed particle size of any 50 release agent particles, and the maximum particle size is determined from any 100 release agent particles.
[0011]
The toner of the present invention may be produced by any method as long as the toner as described above can be obtained. However, by performing a series of steps at a temperature higher than the temperature at which the release agent dissolves in the solvent in a known wet method, the toner of the present invention can be obtained. Toner can be obtained effectively. That is, the toner of the present invention is
(I) a liquid preparation step for preparing an oily phase formed by dissolving and dispersing at least a binder resin or a polymerizable monomer, a colorant and a release agent in an organic solvent;
(II) a granulation step of dispersing the oily phase in the aqueous phase and granulating droplet particles comprising the oily phase; and
(III) a desolvation step of removing the organic solvent from the droplet particles, or (IV) a polymerization-desolubility step of removing the organic solvent from the droplet particles while polymerizing the polymerizable monomer in the droplet particles,
An electrophotography characterized in that the preparation step (I), the granulation step (II), and the desolubilization step (III) or the polymerization-desolubility step (IV) are carried out at a temperature above the temperature at which the release agent dissolves in the solvent The toner can be effectively obtained by the manufacturing method of the toner. In this way, in the wet method, by performing the above step at a temperature higher than the temperature at which the release agent dissolves in the solvent, that is, by performing the above step in a state in which the release agent is dissolved, In the desolubilization process, the release agent is precipitated. At the same time, the viscosity of the droplets increases due to the presence of the dissolved binder resin or the generated binder resin, so that the release agent grows to coarse particles. It is considered that finely dispersed toner can be obtained without aggregation. Even if the release agent is dissolved or finely dispersed in the solvent only in the liquid preparation step (I), the granulation step (II) and the desolubilization step (III) or the polymerization-desolubility step (IV) If the temperature of the release agent is lower than the temperature at which the release agent dissolves in the solvent, the release agent solubility in the solvent decreases, so the release agent that has been finely dispersed grows and aggregates, and the release agent that has been dissolved The agent precipitates, grows and aggregates, and the toner of the present invention cannot be obtained. In particular, when the temperature of the desolubilization process is low, the resin is still dissolved and the release agent abruptly recrystallizes in a state where the viscosity is low as the solvent evaporates.
Hereinafter, the case where the wet method is employed to obtain the toner of the present invention will be described in detail.
[0012]
The toner of the present invention can be obtained by any wet method including no polymerization process or a wet process including a polymerization process.
[0013]
When the toner of the present invention is produced using a wet method that does not include a polymerization process, for example, an emulsion dispersion granulation method,
(I) a liquid preparation step for preparing an oily phase formed by dissolving and dispersing at least a binder resin, a colorant, and a release agent in an organic solvent;
(II) a granulation step of dispersing the oily phase in the aqueous phase and granulating droplet particles comprising the oily phase; and
(III) When performing the desolubilization process to remove the organic solvent from the droplet particles,
The liquid preparation step (I), the granulation step (II), and the desolubilization step (III) can be obtained by performing at or above the temperature at which the release agent dissolves in the solvent.
[0014]
Specifically, first, an oily phase is prepared by dissolving and dispersing at least a binder resin, a colorant and a release agent in an organic solvent (preparation step (I)). In the present invention, the oily phase is prepared at a temperature equal to or higher than the temperature at which the release agent dissolves in the solvent (organic solvent), and the release agent is dissolved in the oily phase. When preparing the oil phase, it is only necessary to prepare an oil phase in which the release agent is dissolved as a result. For example, the toner component may be added to an organic solvent having a predetermined temperature, and mixed and stirred. Alternatively, the toner component may be added to an organic solvent at room temperature and mixed and stirred while heating to a predetermined temperature.
[0015]
The release agent that can be used in the present invention is not particularly limited as long as it can be dissolved in an organic solvent by heating, and known release agents in the field of toners, such as synthetic waxes, natural waxes and waxes, etc. Can be used. Among these release agents, from the viewpoint of improving offset resistance, it is preferable to use a release agent that dissolves in an organic solvent at a temperature of normal temperature to 90 ° C. Specifically, the concentration is 3.5% by weight or more, preferably 10% by weight or more, more preferably 15% by weight or more at a temperature of normal temperature to 90 ° C., preferably 25 to 60 ° C. with respect to the solvent used. It is preferable to use a release agent that dissolves in (release agent / (release agent + solvent)). Further, from the viewpoint of toner heat resistance and low-temperature fixability, the melting point is preferably 60 to 120 ° C.
[0016]
Specifically, as synthetic waxes, for example, synthetic hydrocarbon Fischer-Tropsch, polyethylene, polypropylene and other waxes, modified waxes such as montan, paraffin, microcrystalline, waxes such as esters, fatty acids, acid amides, ketones, etc. Is mentioned. Examples of natural waxes include plant-based carnauba, candelilla and rice waxes, jojoba oil, and the like. Other animal and mineral waxes can also be used. In particular, synthetic waxes such as esters, montans, and ketones, and natural waxes such as carnauba are suitable for the present invention in terms of melting point and solubility in organic solvents.
[0017]
The addition amount of the release agent is preferably 3 to 30 parts by weight, preferably 10 to 25 parts by weight with respect to 100 parts by weight of the binder resin, from the viewpoint of heat resistance and stress resistance of the toner and charging performance. Conventionally, when an amount of wax that can achieve oil-less fixing is added, the OHP translucency deteriorates. However, in the present invention, such a problem does not occur even if a relatively large amount of wax is added as described above. Does not occur.
[0018]
The organic solvent that can be used in the present invention is not particularly limited as long as it is a known organic solvent that can dissolve the release agent. For example, aromatic solvents such as toluene and xylene, and ester solvents such as ethyl acetate and butyl acetate. Ketone solvents such as acetone and methyl ethyl ketone, alcohol solvents such as isopropyl alcohol, n-butanol and ethanol, and halogen solvents such as chloroform and carbon tetrachloride. These organic solvents may be used alone or in admixture of two or more. These solvents are used in a proportion of 50 to 95% by weight in the oily phase as long as they do not adversely affect granulation in the granulation step described later.
[0019]
When using ester wax or carnauba wax as the mold release agent, it is preferable to use toluene as the organic solvent.
[0020]
The temperature at which the oily phase is prepared is not particularly limited as long as the release agent can be dissolved in the organic solvent, and is appropriately selected depending on the type of the release agent and the organic solvent used. Even if the temperature is set too high, it is not preferable from the viewpoint of production efficiency. Therefore, the temperature is usually set within a range of normal temperature to 90 ° C., preferably 25 to 80 ° C. For example, when ester wax or carnauba wax is used as the release agent and toluene is used as the organic solvent, the temperature is preferably 35 to 70 ° C, and preferably 40 to 60 ° C.
[0021]
As the binder resin, resins that can be dissolved in the organic solvent can be used. For example, polyester resins, styrene resins, (meth) acrylic resins, styrene- (meth) acrylic copolymer resins, olefins. It is possible to use one kind or two or more kinds of known various resins such as resin, polyamide resin, polycarbonate resin, polyether resin, polyvinyl acetate resin, polysulfone resin, epoxy resin and polyurethane resin. is there. In the present invention, it is preferable to use a polyester resin from the viewpoint of further fine dispersion of the release agent, solubility in a solvent, toner fixing performance, translucency, and heat resistance. It is more preferable to use a polyester resin having a molecular weight (Mn) of 2000 to 8000, a weight average molecular weight / number average molecular weight (Mw / Mn) of 5 to 20, and a glass transition point of 55 to 70 ° C. Such polyester resins are easily dissolved by the above organic solvents, and even when a release agent is added, the OHP translucency is more effectively maintained, while the low-temperature and high-temperature offset resistance and the fixing performance are effectively improved. It is to do. Further, the heat resistance and stress resistance necessary for the toner are also effectively maintained.
[0022]
In the present invention, when ester wax or carnauba wax is used as a release agent, it is preferable to use a polyester resin as a binder resin. This is because the compatibility between the release agent and the binder resin is good, so that fine dispersion of the release agent is achieved more effectively, and the translucency is further improved because the refractive index of the resin and the wax is close.
[0023]
The colorant is not particularly limited, and a known pigment / dye conventionally used as a colorant for toner can be used.
Examples of the black pigment include carbon black, copper oxide, manganese dioxide, aniline black, activated carbon, nonmagnetic ferrite, magnetic ferrite, and magnetite.
Examples of the yellow pigment include yellow lead, zinc yellow, cadmium yellow, yellow iron oxide, mineral fast yellow, nickel titanium yellow, and benzidine yellow G.
Examples of orange pigments include red chrome yellow, molybdenum orange, permanent orange GTR, parazolone orange, and vulcan orange.
Examples of red pigments include bengara, cadmium red, red lead, mercury sulfide, cadmium, permanent red 4R, risor red, pyrazolone red, watch red, calcium salt, lake red C, lake red D, and brilliant carmine 6B. is there.
[0024]
Examples of blue pigments include bitumen, cobalt blue, alkali blue lake, victoria blue lake, phthalocyanine blue, metal-free phthalocyanine blue, and phthalocyanine blue.
Examples of extender pigments include barite powder, barium carbonate, clay, silica, white carbon, talc, and alumina white.
These colorants can be used alone or in combination of two or more. Usually, it is desirable to use 1 to 20 parts by weight, preferably 2 to 15 parts by weight with respect to 100 parts by weight of the binder resin.
[0025]
A charge control agent may be dissolved or finely dispersed in the oily phase. Any charge control agent (CCA) can be used as long as it can be dissolved or finely dispersed in the organic solvent. Examples of negative charge control agents include metal-containing complex salt Bontron E81, E84 (manufactured by Orient Chemical Co., Ltd.), LR147 (manufactured by Nippon Carlit), thioindigo pigment, calixarene compound Bontron E89 (manufactured by Orient Chemical Co., Ltd.), fluorine-containing compound Compound copy charge NX VP434 (made by Hoechst), FT-310 (made by Neos), etc. are mentioned. Examples of the positive charge control agent include quaternary ammonium salt P-51 (manufactured by Orient Chemical Co.), copy charge PX VP435 (manufactured by Hoechst), and the like. For a color toner, a material which can give positive or negative charge by a triboelectric charge from a transparent color without impairing the color tone is preferable. One or more of these may be used. The addition amount of the charge control agent is not particularly limited, but is 0.1 to 4 parts by weight, preferably 0.5 to 2 parts by weight with respect to 100 parts by weight of the binder resin.
[0026]
Next, the obtained oily phase is dispersed in the aqueous phase to granulate droplet particles composed of the oily phase (granulation step (II)). That is, a dispersion system (O / W emulsion) in which liquid particles comprising an oily phase are dispersed in an aqueous phase is prepared. In the present invention, granulation is performed at a temperature at which the release agent dissolved in the droplets does not precipitate, that is, at a temperature higher than the temperature at which the release agent dissolves in the solvent (organic solvent). Usually, granulation is performed while maintaining the temperature of the liquid preparation process. Therefore, at the time of dispersion, it is preferable that the oily phase and the aqueous phase are respectively controlled at a predetermined temperature, and then mixed, dispersed and granulated.
[0027]
In granulation, the oily phase may be added to the aqueous phase and emulsified, and the oily phase may be dispersed in the aqueous phase, or the aqueous phase may be added to the oily phase and phase-inverted and emulsified to make the oily phase aqueous. It may be dispersed in the phase.
[0028]
The aqueous phase is formed by adding an additive such as a dispersant and / or a dispersion aid to water as required. The dispersant is preferably a hydrophilic colloid in the aqueous phase, particularly gelatin, gum arabic, agar, cellulose derivatives, synthetic polymers (eg, polyvinyl alcohol, polyvinyl pyrrolidone, polyacrylate, polymethacrylate, etc.). Insoluble inorganic salts (for example, calcium phosphate), hydrophilic silica and the like. A surfactant is usually used as a dispersion aid, a natural surfactant such as aponin, a nonionic surfactant such as alkylene oxide, glycerin or glycidol, carboxylic acid, sulfonic acid, phosphoric acid, sulfate ester group, Examples include anionic surfactants containing acidic groups such as phosphate ester groups.
[0029]
The concentration of the dispersant and the dispersion aid in the aqueous phase is not particularly limited, and generally 1 to 10% by weight and 0.001 to 1% by weight are preferable, respectively.
[0030]
When dispersing the oily phase in the aqueous phase, it is preferable to control the diameter of the liquid particles in the oily phase by stirring so that the toner particles obtained have a desired particle size. The mixing volume ratio of the oily phase to the aqueous phase (oily phase / aqueous phase) can be selected between 1/1 to 1/4 in consideration of the emulsion stability.
[0031]
After granulating the droplet particles composed of the oil phase, the organic solvent is removed from the droplet particles (demelting step (III)). Desolubilization may be performed at a temperature at which the release agent does not precipitate due to a decrease in the solubility of the release agent in the organic solvent as the temperature in the system decreases. Usually, the release agent is a solvent (organic solvent). It is carried out over a long time while maintaining the temperature of the preparation step. In this way, by performing the desorption while avoiding the precipitation of the release agent due to a decrease in system temperature (decrease in solubility), only the release agent is precipitated due to solvent removal, and at the same time, the dissolution in the droplet particles Therefore, it is considered that the release agent fine particles precipitated in the toner can be finely dispersed without growing or agglomerating.
[0032]
In the present invention, it is preferable to perform the demelting step over a long time. This is because the release agent can be finely dispersed more effectively. Since it differs with each kind of organic solvent, mold release agent, and resin, it cannot be limited.
[0033]
After the removal of the organic solvent is completed, the toner of the present invention can be obtained by cooling, repeating filtration / washing several times, drying and crushing.
[0034]
The toner of the present invention can also be obtained by employing a wet method including a polymerization process, such as a suspension polymerization method, an emulsion polymerization method, an emulsion polymerization aggregation method, a seed polymerization method, and an interfacial polymerization method. Hereinafter, the case where the toner of the present invention is obtained by adopting a wet method including a polymerization process will be described. However, unless otherwise specified, the same process as in the case of employing the wet method not including the polymerization process is used. In the wet process including a polymerization process, the polymerizable monomer also acts as a “solvent”, and therefore “solvent” means “a mixed solvent of an organic solvent and a polymerizable monomer”. Further, regarding the addition amount, “100 parts by weight of the binder resin” is read as “100 parts by weight of the polymerizable monomer”.
[0035]
When the toner of the present invention is produced using a wet method including a polymerization process, particularly a suspension polymerization method,
(I) a liquid preparation step for preparing an oily phase obtained by dissolving / dispersing at least a polymerizable monomer, a colorant and a release agent in an organic solvent;
(II) a granulation step of dispersing the oily phase in the aqueous phase and granulating droplet particles comprising the oily phase; and
(IV) In performing the polymerization-desolubilization step of removing the organic solvent from the droplet particles while polymerizing the polymerizable monomer in the droplet particles,
The liquid preparation step (I), the granulation step (II), and the polymerization-desolubilization step (IV) can be obtained by performing at or above the temperature at which the release agent dissolves in the solvent.
[0036]
Specifically, first, an oily phase is prepared by dissolving and dispersing at least a polymerizable monomer, a colorant, and a release agent in an organic solvent (preparation step (I)). In the wet method including a polymerization process, the oily phase is prepared at a temperature higher than the temperature at which the release agent dissolves in the solvent, that is, the mixed solvent of the organic solvent and the polymerizable monomer, and the release agent is dissolved in the oily phase. Yes.
[0037]
The organic solvent is usually used at a ratio of 5% by weight or more in the oily phase, but may not be used. When no organic solvent is used, the oily phase is prepared above the temperature at which the release agent dissolves in the polymerizable monomer.
[0038]
The polymerizable monomer is not particularly limited as long as it can constitute the binder resin and has hydrophobicity. For example, styrene resin, (meth) acrylic resin, styrene- (meth) acrylic copolymer Examples thereof include vinyl monomers that are raw materials for resins and the like.
[0039]
It is preferable that a polymerization initiator is added to the oily phase. As a polymerization initiator, radical polymerization initiators, such as an azo compound type, a hydroperoxide type, and a redox type, are mentioned, for example.
[0040]
Next, the obtained oily phase is dispersed in the aqueous phase to granulate droplet particles composed of the oily phase (granulation step (II)). In the present invention, granulation is performed at a temperature at which the release agent dissolved in the droplets does not precipitate, that is, the temperature at which the release agent is dissolved in a solvent (a mixed solvent of an organic solvent and a polymerizable monomer). This is done. Usually, granulation is performed while maintaining the temperature of the liquid preparation process. In the case where no organic solvent is used, the granulation is performed at a temperature higher than the temperature at which the release agent dissolves in the polymerizable monomer.
[0041]
Next, the organic solvent is removed from the droplet particles while polymerizing the polymerizable monomer in the droplet particles (polymerization-desolubilization step (IV)). That is, in this process, desorption is performed while polymerization is performed, and as a result, the desorption is completed at the end of the polymerization.
[0042]
Polymerization-desolubilization is performed at a temperature at which the release agent does not precipitate due to a decrease in release agent solubility accompanying a decrease in system temperature, that is, the release agent is a solvent (organic solvent and polymerizable monomer). At a temperature equal to or higher than the temperature at which the solvent is dissolved. In the case where no organic solvent is used, the polymerization / dissolution is performed at a temperature equal to or higher than the temperature at which the release agent is dissolved in the polymerizable monomer. In this way, by performing polymerization-desolubility while avoiding precipitation of the release agent due to a decrease in system temperature (decrease in solubility), only removal of the solvent and precipitation of the release agent due to resin formation occur at the same time. It is considered that the release agent fine particles deposited in the toner can be finely dispersed without growing or aggregating because the viscosity is increased by removing the solvent and generating the resin in the droplet particles.
[0043]
Specifically, the conditions such as the temperature and time of the polymerization-demelting step are not particularly limited as long as the above requirements are satisfied with respect to the temperature, but have the Mn, Mw / Mn and glass transition point described in the description of the binder resin. It is preferable that the conditions are such that a resin is obtained.
[0044]
In the present invention, it is preferable to perform the polymerization-desolubilization process over a long period of time. This is because the release agent can be finely dispersed more effectively.
[0045]
After the removal of the organic solvent is completed, the toner of the present invention can be obtained by cooling, repeating filtration / washing several times, drying and crushing.
[0046]
The toner of the present invention that can be produced by the above production method is desirably controlled to have a volume average particle diameter of 3 to 10 μm, preferably 4 to 8 μm.
[0047]
The toner of the present invention is preferably surface-treated with fine particles from the viewpoint of improving fluidity, chargeability, heat resistance and the like. As the fine particle material, conventionally known fine particle materials externally added to toner in the field of electrophotography can be used, and examples thereof include metal oxides, intermetallic compounds, and resins. Specific examples of the metal oxide include silica, titanium oxide, alumina, and zirconia. Examples of the intermetallic compound include strontium titanate, silicon carbide, silicon nitride, and the like. Examples of the resin include a polymer fluoride, a silicone compound, an acrylic resin, and the like. The addition amount of the fine particles is suitably 0.2 to 3 parts by weight with respect to 100 parts by weight of the toner.
[0048]
Since the toner of the present invention can contain a relatively large amount of a release agent in a finely dispersed state, the object of the present invention can be effectively achieved even when used in a copying machine employing an oilless fixing method.
[0049]
The toner of the present invention can be used as a two-component developing toner used with a carrier or as a one-component developing toner not using a carrier.
[0050]
As the carrier used with the toner of the present invention, a known carrier can be used. For example, a carrier made of magnetic particles such as iron powder and ferrite, and a coated carrier in which the surface of the magnetic particles is coated with a coating agent such as a resin. Alternatively, any of a dispersion type carrier in which a magnetic fine powder is dispersed in a binder resin can be used.
Hereinafter, the present invention will be described in more detail with reference to examples.
[0051]
【Example】
Example 1
Number average molecular weight Mn is 2,800, weight average molecular weight / number average molecular weight (Mw / Mn) is 7, and Tg is 68 ° C. ) Put together with 0.5g in a 2 liter plastic bottle, mix and disperse with Ultra Turrax (IKA) for 30 minutes, then add 20g of ester wax HOE-WAX F (Clariant) with a melting point of 80 ° C to 50 ° C Then, an oily phase in which wax was dissolved in toluene was prepared by heating. Next, 11 g of sodium alkyldiphenyl ether disulfonate is added to 1100 g of a 3.5 wt% aqueous solution of sodium polyacrylate to prepare an aqueous phase at 50 ° C., and this is mixed in an oily phase maintained at 50 ° C. Was kept at 50 ° C. and emulsified by stirring at 3500 rpm for 10 minutes with a TK auto homomixer (manufactured by Tokushu Kika Kogyo Co., Ltd.). Immediately, the mixture was stirred for 20 hours with a three-one motor in a thermostatic bath at 50 to 55 ° C. to remove toluene, and after cooling, filtration / washing was repeated several times. The washed toner cake is transferred to a stainless steel vat, dried at 35 ° C for 48 hours in a constant temperature dryer, crushed using a ball mill, and sieved with a 90 µm mesh to obtain a toner with an average particle size of 6.2 µm. It was. As a result of observation with a transmission electron microscope (50,000 times) (hereinafter the same), wax particles having an average particle diameter of 0.05 μm and a maximum particle diameter of 0.23 μm were dispersed inside the toner particles.
[0052]
(Example 2)
A toner having an average particle size of 7.5 μm was obtained in the same manner as in Example 1 except that 10 g of Carnauba 45T-1 (manufactured by Seiro Co., Ltd.) having a melting point of 93 ° C. was used as the wax. Wax particles having an average particle size of 0.08 μm and a maximum particle size of 0.37 μm were dispersed inside the toner particles.
[0053]
Example 3
A toner having an average particle size of 5.4 μm was obtained in the same manner as in Example 1 except that polyester having Mn of 3000, Mw / Mn of 9 and glass transition point of 60 ° C. was used as the binder resin. Wax particles having an average particle size of 0.04 μm and a maximum particle size of 0.18 μm were dispersed inside the toner particles.
[0054]
(Comparative Example 1)
A toner having an average particle size of 7.0 μm was obtained in the same manner as in Example 1 except that 20 g of n-hexadecyl ether having a melting point of 55 ° C. was used as the wax. Wax particles having an average particle size of 1.5 μm and a maximum particle size of 4.8 μm were dispersed inside the toner particles.
[0055]
(Comparative Example 2)
A toner having an average particle size of 8.6 μm was obtained in the same manner as in Example 1 except that 2 g of polyethylene wax 400P (manufactured by Mitsui Chemicals) having a melting point of 126 ° C. was used as the wax. Wax particles having an average particle size of 3.5 μm and a maximum particle size of 6.2 μm were dispersed inside the toner particles.
[0056]
Table 1 summarizes the type, melting point, addition amount and concentration of the wax used in each example and comparative example, and the saturated concentration of each wax with respect to toluene at each temperature.
[0057]
[Table 1]
[0058]
100 parts by weight of the toner obtained in the above Examples and Comparative Examples was subjected to surface treatment for 3 minutes at a speed of 30 m / s with 1.2 parts by weight of silica fine particles R972 (manufactured by Nippon Aerosil Co., Ltd.) using a Henschel mixer (manufactured by Mitsui Metal Mining). went. A two-component nonmagnetic developer was obtained by mixing with a carrier described later at a toner mixing ratio of 6% by weight, and each developer was evaluated for the following evaluation items.
[0059]
(Non-offset temperature range)
A fixing tester that modifies the fixing device of the full-color copier CF900 (manufactured by Minolta Co., Ltd.) and variably controls the fixing temperature to enable paper passing and fixing is used. After copying with a fixing tester, fixing was performed at various fixing temperatures. After one rotation of the roller, it was visually evaluated whether the offset toner image stained the copy paper, and the upper and lower temperatures without contamination were measured. The wider these temperature ranges, the better.
[0060]
(Translucent)
Using the fixing tester, a copy image on OHP paper fixed at the center temperature in the non-offset temperature range was visually evaluated with an overhead projector EZ-2 (Fuji Photo Film Co., Ltd.).
○: Transparent and good without turbidity;
X: Opaque and practically unusable.
[0061]
The results are shown in the table below.
[Table 2]
[0062]
Using each developer, 10,000 copies were made with CF900 (Minolta Co., Ltd.), and the developer and copied images after the initial and 10,000 copies were evaluated.
(Charge amount)
In the electric field separation type charge amount measuring apparatus shown in FIG. 1, 2 g of developer is coated on the
[0063]
(Image density)
The density of any 10 points in the solid copy image with the maximum density by CF900 (manufactured by Minolta) was measured with a Macbeth densitometer (manufactured by Macbeth), and the average value x was obtained and evaluated according to the following.
○: 1.0 <x <1.3
Δ: 0.8 <x ≦ 1.0 or 1.3 ≦ x <1.5
X: x ≦ 0.8 or 1.5 ≦ x
[0064]
(Granularity)
A copy image by CF900 (manufactured by Minolta) was visually observed, and the graininess was evaluated according to the following ranking. Note that the granularity means the uniformity of a solid image with a low density (quality of texture).
○: It was good without being inferior to the original
Δ: Slightly inferior to the original, but no problem in practical use;
X: It was considerably inferior to the original and could not be used practically.
[0065]
(Skin fog)
Copy images by CF900 (Minolta) were visually observed, and background fog was evaluated according to the following ranking. The background fogging refers to a stain caused by toner generated by developing and transferring low-charge / reverse-charge toner on a copy sheet in addition to the original image portion.
○: Good without fogging;
Δ: Although there was fog, there was no problem in practical use;
X: Unusable for practical use.
[0066]
The results are shown below.
[Table 3]
[0067]
Career
Polyester resin Byron 200 (manufactured by Toyobo Co., Ltd.) was dissolved in a mixed solvent of toluene and isopropanol, applied to a sintered ferrite powder F300 (manufactured by Powder Tech Co.) having an average diameter of 40 μm with a Spiracoater (manufactured by Okada Seiko Co., Ltd.) and dried. After firing in an oven at 140 ° C. for 2 hours, crushing and sieving were carried out to prepare a polyester resin-coated ferrite carrier having an average diameter of 42 μm.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram of a charge amount measuring apparatus used for measuring a charge amount.
[Explanation of symbols]
1: cylindrical electrode, 2: conductive sleeve, 3: magnetic roll, 4: bias electrode, 5: capacitor for measurement, 6: developer, 7: separated toner.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000062146A JP3770036B2 (en) | 2000-03-07 | 2000-03-07 | Toner for electrophotography and method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000062146A JP3770036B2 (en) | 2000-03-07 | 2000-03-07 | Toner for electrophotography and method for producing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2001249487A JP2001249487A (en) | 2001-09-14 |
| JP3770036B2 true JP3770036B2 (en) | 2006-04-26 |
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| JP2000062146A Expired - Fee Related JP3770036B2 (en) | 2000-03-07 | 2000-03-07 | Toner for electrophotography and method for producing the same |
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| JP (1) | JP3770036B2 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP6862149B2 (en) * | 2016-11-14 | 2021-04-21 | キヤノン株式会社 | Toner manufacturing method |
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| Publication number | Publication date |
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| JP2001249487A (en) | 2001-09-14 |
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